Metal halide redox flow battery

• US 20050244707A1
• Filed: 04/23/2003
• Published: 11/03/2005
• Est. Priority Date: 04/23/2002
• Status: Abandoned Application

• Current Assignee: NewSouth Innovations Pty Limited (University Of New South Wales)
• Original Assignee: NewSouth Innovations Pty Limited (University Of New South Wales)
• Inventors: Mousa, Asem, Kazacos, Michael, Skyllas-Kazacos, Maria
• Application Number:
  US10/512,417
• Publication Number:
  US 20050244707A1
• Time in Patent Office: Days
• US Class Current: 429/105
• CPC Class Codes: B60L 58/34 by heating
• CPC Class Codes: H01M 12/08 composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
• CPC Class Codes: H01M 8/188 by recharging of redox couples containing fluids; Redox flow type batteries
• CPC Class Codes: H01M 8/20 Indirect fuel cells, e.g. fuel cells with redox couple being irreversible H01M8/18 takes precedence
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02E 60/50 Fuel cells
• CPC Class Codes: Y02T 90/40 Application of hydrogen technology to transportation, e.g. using fuel cells

Abstract

A 3 M V(IV) bromide solution in 3-4 M HBr or HBr/HCl mixture is added to both sides of the redox flow cell or battery. On fully charging the cell, the vanadium (IV) bromide solution is reduced to produce 3M VBr₂ in the negative half-cell, while the bromide ions in the positive half-cell are oxidised to produce 1.5 M Br₃— or ClBr₂. On discharge, the VBr₂ is oxidised to VBr₃ in the negative half cell while the Br₃ or ClBr₂— ions are reduced to Br ions in the positive half cell. The cell comprises carbon or graphite felt bonded onto plastic or conducting plastic sheets as substrate materials and the two half cells are separated by an anion or cation exchange membrane.

Claims

1. A metal halide redox flow cell comprising:

a negative half-cell having;

an electrolyte containing a two valency state metal redox couple and

a positive half-cell having;

an electrolyte containing halide redox couple;

wherein the positive half-cell electrolyte also contains;

a halide of the said metal to provide substantial equilibrium of metal ion migration between the half cells.

2. A redox flow cell as claimed in claim 1, wherein the metal is chosen from the group consisting of vanadium, copper, molybdenum, manganese, tin and titanium.

3. A redox flow cell as claimed in claim 2, wherein the two valency state metal redox couple is chosen from the group consisting of the V(II)/V(III) couple, the Cu(I)/Cu(II) couple, the Mo(II)/Mo(III) couple, the Mn(II)/Mn(III) couple, the Sn(II)/Sn(IV) couple and the Ti(III)/Ti(IV) couple.

4. A redox flow cell as claimed in claim 1, wherein the halide redox couple comprises bromine.

5. A redox flow cell as claimed in claim 4, wherein the halide redox couple comprises one or more (as mixtures) of the following halide and polyhalide/halide redox couples

Br₃⁻

/Br⁻

,

ClBr₂⁻

/Br⁻

,

BrCL₂³¹ /Cl⁻

.

6. A redox flow cell as claimed in claim 5, wherein the halide redox couple comprises Br₃⁻

/Br⁻

and a supporting electrolyte in each half-cell comprises HBr, NaBr, KBr or mixtures thereof in a concentration range from 0.1 M to 12 M.

7. A redox flow cell as claimed in claim 5, wherein the halide redox couple comprises ClBr₂⁻

/Br⁻

or BrCL₂⁻

/Cl⁻

and a supporting electrolyte in each half-cell comprises HCI, NaCl or KCl or mixtures thereof in a concentration range from 0.5 M to 6 M to form stable polyhalides with the bromine that is formed in the positive half-cell during charging.

8. A redox flow cell as claimed in claim 4, wherein said method is chosen from the group consisting of vanadium, copper, molybdenum, manganese, tin and titanium and the concentration of said metal bromides in the negative and positive half-cell electrolytes is from 0.1 M to 6 M.

9. A redox flow cell as claimed in claim 8, wherein the concentration of said metal bromides in the negative and positive half-cell electrolytes is from 0.5 M to 5 M.

10. A redox flow cell as claimed in claim 9, wherein the concentration of said metal bromides in the negative and positive half-cell electrolytes is from 1 M to 4 M.

11. A redox flow cell as claimed in claim 5, wherein the concentration of Br₃⁻

, Br₂Cl⁻

and/or Cl₂Br⁻

ions in the positive half cell of the fully charged vanadium, copper, molybdenum, manganese, tin or titanium bromide redox flow cell is between 0.1 M to 5 M.

12. A redox flow cell as claimed in claim 11, wherein the concentration of Br₃⁻

, Br₂Cl⁻

and/or Cl₂Br⁻

ions in the positive half cell of the fully charged vanadium, copper, molybdenum, manganese, tin or titanium bromide redox flow cell is between 1 M to 3 M.

13. A redox flow cell as claimed in claim 4, including a solution of 0.1 M to 5 M charged vanadium, copper, molybdenum, manganese, tin or titanium bromide in both half-cells.

14. A redox flow cell as claimed in claim 2, wherein the metal is vanadium and when the cell is discharged, the vanadium in the negative half-cell is in V(III) and/or V(IV) state in a supporting electrolyte selected from the group consisting of HBr, NaBr, KBr and mixtures thereof and the vanadium in the positive half-cell is in V(IV) and/or V(V) state also in a supporting electrolyte selected from the group consisting of HBr, NaBr, KBr and mixtures thereof.

15. A redox flow cell as claimed in claim 14, wherein the positive and negative half cell electrolytes also contain chloride ions at a concentration of 0.1 M to 5 M.

30. A redox flow cell of claim 1, wherein the two half-cell electrolytes are separated by an ion exchange membrane which prevents the bulk mixing of the solutions in the two half cells as they are pumped through the cell.

31. A redox flow cell as-claimed in claim 30, wherein the ion exchange membrane is a cation exchange membrane adapted to allow the transfer of charge carrying H⁺, Na⁺ and/or K⁺ ions.

32. A redox flow cell as claimed in claim 31, wherein the ion exchange membrane is an anion exchange membrane adapted to allow the transfer of charge carrying H⁺ Br⁻

and/or Cl⁻

ions.

33. A redox flow cell as claimed in claim 31, wherein the ion exchange membrane is chosen from the group consisting of Nafion 112, Nafion 117, other Nafion cation exchange membranes, Gore Select membranes, Flemion membranes and Selemion CMV cation exchange membranes.

34. A redox flow cell as claimed in claim 1, including negative and positive electrodes of porous carbon or graphite felt, matte or cloth materials on a graphite, glassy carbon or conducting plastic substrate.

35. A redox flow cell as claimed in claim 1, wherein the positive electrode material is an oxide coated titanium metal sheet or expanded metal mesh.

46. A redux flow cell as claimed in claim 6, wherein said concentration range is 0.1 M to 8 M.

47. A redux flow cell as claimed in claim 12, wherein said concentration range is 1 M to 2 M.

16. A method of producing a metal halide redox flow cell comprising a negative half-cell having an electrolyte containing a two-valency-state metal redox couple and a positive half-cell having an electrolyte containing halide redox couple and a halide of the said metal, the method consisting in the steps of:

adding to both half cells;

a solution of a salt of a halide&

of the said metal and

a supporting electrolyte comprising hydro-halic acid and/or a salt of one or more Group I metal halide(s) and

charging the cell.

17. A method as claimed in claim 16, wherein the metal is chosen from the group consisting of vanadium, copper, molybdenum, manganese, tin and titanium.

18. A method as claimed in claim 16, wherein the metal in the halide salt of the said metal as added in the second step is in a higher valency state than its two valency states in its redox couple.

19. A method as claimed in claim 18, wherein said metal is vanadium and its redox couple valency states are V(II)V(III) and its said higher valency state is V(IV).

20. A method as claimed in claim 18, wherein said salt is a vanadium bromide.

21. A method as claimed in claim 20, wherein the solution is of 0.1 M to 5 M V(IV) bromide.

22. A method as claimed in claim 16, wherein the supporting electrolyte comprises hydrobromic acid, sodium bromide or potassium bromide or mixtures thereof.

23. A method as claimed in claim 22, wherein the supporting electrolyte includes hydrochloric acid, sodium chloride or potassium chloride or mixtures thereof.

24. A redox flow cell produced by the method of claim 16, wherein the said two valency state metal is vanadium and during cycling of the cell, the negative half-cell electrolyte comprises V(II), V(III) and/or V(IV) ions and the positive electrolyte comprises a bromide/polyhalide couple in the presence of V(IV) and/or V(V) ions.

25. A redox flow cell as claimed in claim 24, wherein, during cycling, the negative half-cell electrolyte contains VBr₂ and/or VBr₃ in a supporting electrolyte selected from the group HBr, NaBr, KBr, HCl, NaCl, KCl or mixtures thereof.

26. A redox flow cell as claimed in claim 25, wherein, during cycling, the negative half cell electrolyte solution comprises 0.5 M to 5 M VBr₃ and/or VBr₂ in 0.1 M to 10 M HBr or HCl/HBr or NaCl/HBr or KCl/HBr mixtures.

27. A redox flow cell provided by the method of claim 16, wherein, when discharged, the positive half-cell electrolyte solution that includes ions of the said metal in a mixture of Cl⁻

and Br⁻

of total concentration 1 M to 12 M; and

, when charged, the positive half-cell electrolyte includes ions of the said metal in a solution containing 0.5 M to 5 M Br₃⁻

or Br₂Cl⁻

ions or mixtures thereof.

28. A redox flow cell as claimed in claim 25, wherein the negative half-cell electrolyte solution contains an excess bromide and chloride ion concentration of 0.1 M to 10 M.

29. A redox flow cell as claimed in claim 25, wherein the said two valency state metal is vanadium and the discharged or partially charged positive half-cell electrolyte solution comprises V(IV) and/or V(V) ions in a supporting electrolyte of HBr, NaBr, KBr or mixture, at a concentration of 0.5 M to 5 M vanadium ions in a mixture of 0.5 M to 12 M bromide and chloride ions.

48. A method as claimed in claim 22, wherein the concentration of the hydrobromic acid, sodium bromide or potassium bromide or mixture thereof is 0.5 M to 10 M.

49. A method according to claim 23, wherein the concentration of the hydrochloric acid, sodium chloride or potassium chloride or mixtures thereof is 0.1 M to 5 M.

50. A redux flow cell as claimed in claim 28, wherein the excess bromide and chloride ion concentration is 0.1 M to 5 M.

36. An electrolyte solution for use in both half-cells of a vanadium bromide redox flow cell, the solution comprising 0.5 M to 5 M V(IV) bromide in a supporting electrolyte of HBr, NaBr, KBr or mixtures thereof.

37. An electrolyte solution as claimed in claim 36, including chloride ions at a concentration of 0.1 M to 5 M.

38. A negative half-cell, electrolyte solution for a vanadium bromide redox flow cell, comprising 0.5 M to 5 M VBr₂ and/or VBr₃ in a supporting electrolyte of HBr, NaBr, KBr or mixtures thereof.

39. A negative half-cell electrolyte solution as claimed in claim 38, including Cl⁻

ions at a concentration of 0.1 M to 5 M.

40. A negative half-cell electrolyte as claimed in claim 39, in which there is an excess bromide and chloride ion concentration of 0.1 M to 10 M.

51. A negative half-cell electrolyte as claimed in claim 40, wherein said concentration is 0.1 M to 5 M.

41. A discharged or partially charged positive half-cell electrolyte solution for vanadium bromide redox flow cell, comprising V(IV) and/or V(V) ions in a supporting electrolyte of HBr, NaBr, KBr or mixture thereof.

42. A positive half-cell electrolyte as claimed in claim 41, wherein the concentration is of 0.5 M to 5 M vanadium ions in a mixture of 0.5 M to 12 M bromide and chloride ions.

43. A method for producing an electrolyte for a vanadium bromide redox, comprising the steps of mixing of equimolar amounts of a V(III) compound with a V(V) compound in a solution of HBr, NaBr, KBr or mixtures thereof and stirring until fully dissolved.

44. A method as claimed in claim 43, wherein the V(III) compound is V₂O₃ and the V(V) compound is V₂O₅.

45. A method as claimed in claim 43, wherein said solution also contains chloride ions.